US11286183B2ActiveUtilityA1
System and method for treatment of spent caustic wastewater
Est. expiryNov 19, 2035(~9.3 yrs left)· nominal 20-yr term from priority
C02F 9/00C02F 2101/38C02F 2103/365C02F 2101/345C02F 2101/32C02F 2101/10C02F 2303/02C02F 1/78C02F 1/30C02F 2101/40C02F 1/66C02F 1/725C02F 1/36
25
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Cited by
60
References
11
Claims
Abstract
The present disclosure relates to a process for treating and regenerating a spent caustic solution at ambient temperatures and pressure which includes oxidizing spent caustic wastewater with a brine solution and ozone mixture, supported by irradiation of the spent caustic wastewater by ultrasound. A range of wastewater treatment techniques may also be included to reach a desired effluent quality level.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1. A system for treating spent caustic wastewater comprising:
a treatment system including:
a brine mixture and oxygen treatment apparatus configured to mix a brine mixture and ozone with the spent caustic wastewater, wherein the spent caustic wastewater comprises greater than 10 ppm total sulfide content;
a pH adjustment apparatus configured to mix acid with the spent caustic wastewater; and
an agitator for providing a mechanical catalyst to an output of the oxygen treatment apparatus; and
an ultrasound apparatus to assist in accelerating chemical reactions between the spent caustic wastewater, the brine mixture and ozone;
wherein the combination of the brine mixture, ozone and spent caustic wastewater and the mechanical catalyst produce a treated wastewater, wherein the treated wastewater comprises less than 10 ppm total sulfide content;
wherein the brine mixture is a combination of a halogen and an alkaline component; and
wherein the alkaline component is ammonia (NH 3 ).
2. The system of claim 1 wherein the halogen is selected from the group consisting of fluorine (F), chlorine (Cl), bromine (Br) and iodine (I).
3. The system of claim 1 further comprising a coolant pump for cooling the treated wastewater.
4. The system of claim 1 further comprising:
a wastewater tank, connected to an input of the treatment system, for holding the spent caustic wastewater; and
a holding tank, connected to an output of the treatment system, for holding the treated wastewater.
5. The system of claim 4 further comprising a pump for pumping the spent caustic wastewater from the wastewater tank to the holding tank.
6. The system of claim 5 further comprising:
a brine mixture tank for storing the brine mixture for use by the brine mixture and ozone treatment apparatus;
an oxygen generator for storing ozone for use by the brine mixture and oxygen treatment apparatus; and
an acid tank for storing acid for use by the pH adjustment apparatus.
7. A method of treating spent caustic wastewater comprising:
mixing a halogen with an alkaline component to produce a brine mixture;
mixing the brine mixture with the spent caustic wastewater wherein the spent caustic wastewater comprises greater than 10 ppm total sulfide content;
adding ozone to the spent caustic wastewater;
applying a mechanical catalyst to a combination of the brine mixture, ozone and the spent caustic wastewater; and
applying an ultrasound cavitation to the combination of the brine mixture, ozone and the spent caustic wastewater to produce a treated wastewater, wherein the treated wastewater comprises less than 10 ppm total sulfide content;
wherein the alkaline component is ammonia (NH 3 ).
8. The method of claim 7 further comprising:
adding an acid to balance a pH of the combination to produce a treated wastewater.
9. The method of claim 8 wherein the halogen is selected from the group consisting of fluorine (F), chlorine (Cl), bromine (Br) and iodine (I).
10. The method of claim 7 wherein the brine mixture and the ozone are mixed together before being added to the spent caustic wastewater.
11. The method of claim 7 wherein the brine mixture and the ozone are added to the spent caustic wastewater concurrently.Cited by (0)
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